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US3240695A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for refining petroleum fractions

Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1963-12-09
•
Granted: 1966-03-15
•
Expires: 1983-12-09
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Abstract

No abstract record available.

Inventors

  • 👤 Hamner Glen Porter
  • 👤 Jones Thomas Garrett
  • 👤 Denbo Robert Thomas
  • 👤 Lindsey Paul Carpenter

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-06 12:51
CPC Classifications
C; C10; C10G; C10G47/00

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 292 words
A PROCESS FOR UPGRADING THE MID-BOILING FRACTIONS OF PETROLEUM CRUDE OIL WHICH COMPRISES FLASHING A TOPPED CRUDE OIL UNDER VACUM AT A FLASH TEMPERATURE ABOVE ABOUT 900*F. (EVUIVALENT AT 760 MM. HG) TO PRODUCE A HEAVY GAS OIL FRACTION HAVING A BOILING RANGE OF ABOUT 500 TO 1050*F., CATALYTICALLY CRACKING SAID HEAVY GAS OIL FRACTION IN ONE-PASS CATALYTIC CRACKING ZONE AT A TEMPERATURE BETWEEN 750 AND 1050*F., DISTILLING THE CATALYTICALLY CRACKED PRODUCT TO SEPARATE FURNACE OIL AND LIGHTER FRACTIONS AND A HEAVY RESIDENTIAL FRACTINAND PRODUCE A CYCLE OIL FRACTION BOILING WITHIN THE RANGE OF ABOUT 400* TO 750* F., PASSING SAID CYCLE OIL TO A STEAM CRACKER, STEAM CRACK ING SAID CYCLE OIL AT A LOW PRESSURE AND AT A TEMPERATURE BETWEEN 1100 AND 1500*F. AND A HOLDING TIME OF 0.1 TO 2.5 SECONDS, DISTILLING THE STEAM CRACKED PRODUCT TO SEPARATE HYDROCARBONS BOILING AT ABOUT 450*F. OR LESS AND TO PRODUCE A SIDE STREAM FRACTION BOILING BETWEEN 450 AND 650*F. AND A TAR BOTTOMS FRACTION BOILING ABOVE ABOUT 650*F. AND UP TO ABOUT 1200*F., CONTACTING SAID SIDE STREAM FRACTION WITH HYDROGEN IN AT LEAST ONE HYDROCRACKING STAGE IN THE PRESENCE OF A HYDROCRACKING CATALYST AT A TEMPERATURE BETWEEN 550 AND 800*F. AND DISTILLING THE RESULTING HYDROCRACKED PRODUCT TO SEPARATE A RESIDUE FRACTION FROM A PRODUCT GASOLINE FRACTION, PASSING SAID TAR BOTTOMS FRACTION RESULTING FROM THE DISTILLATION OF SAID STEAM-CRACKED PRODUCT INTO A THERMAL SOAKING ZONE, SUBJECTING SAID TAR BOTTOMS FRACTION TO A TEMPERATURE BETWEEN 750 AND 950*F. FOR A PERIOD OF FROM 2 TO 6 HOURS TO CONVERT SAID TAR BOTTOMS TO PITCH AND MORE VOLATILE PRODUCTS, PASSING SAID PITCH AND VOLATILE PRODUCTS TO A DISTILLATION ZONE AND THERIEN STRIPPING THE PITCH OF SUBSTANTIALLY ALL THE VIOLATE PRODUCTS BOILING BELOW ABOUTG 750*F.
Claim 2
Dependent Claim 292 words
A PROCESS FOR UPGRADING THE MID-BOILING FRACTIONS OF PETROLEUM CRUDE OIL WHICH COMPRISES FLASHING A TOPPED CRUDE OIL UNDER VACUM AT A FLASH TEMPERATURE ABOVE ABOUT 900*F. (EVUIVALENT AT 760 MM. HG) TO PRODUCE A HEAVY GAS OIL FRACTION HAVING A BOILING RANGE OF ABOUT 500 TO 1050*F., CATALYTICALLY CRACKING SAID HEAVY GAS OIL FRACTION IN ONE-PASS CATALYTIC CRACKING ZONE AT A TEMPERATURE BETWEEN 750 AND 1050*F., DISTILLING THE CATALYTICALLY CRACKED PRODUCT TO SEPARATE FURNACE OIL AND LIGHTER FRACTIONS AND A HEAVY RESIDENTIAL FRACTINAND PRODUCE A CYCLE OIL FRACTION BOILING WITHIN THE RANGE OF ABOUT 400* TO 750* F., PASSING SAID CYCLE OIL TO A STEAM CRACKER, STEAM CRACK ING SAID CYCLE OIL AT A LOW PRESSURE AND AT A TEMPERATURE BETWEEN 1100 AND 1500*F. AND A HOLDING TIME OF 0.1 TO 2.5 SECONDS, DISTILLING THE STEAM CRACKED PRODUCT TO SEPARATE HYDROCARBONS BOILING AT ABOUT 450*F. OR LESS AND TO PRODUCE A SIDE STREAM FRACTION BOILING BETWEEN 450 AND 650*F. AND A TAR BOTTOMS FRACTION BOILING ABOVE ABOUT 650*F. AND UP TO ABOUT 1200*F., CONTACTING SAID SIDE STREAM FRACTION WITH HYDROGEN IN AT LEAST ONE HYDROCRACKING STAGE IN THE PRESENCE OF A HYDROCRACKING CATALYST AT A TEMPERATURE BETWEEN 550 AND 800*F. AND DISTILLING THE RESULTING HYDROCRACKED PRODUCT TO SEPARATE A RESIDUE FRACTION FROM A PRODUCT GASOLINE FRACTION, PASSING SAID TAR BOTTOMS FRACTION RESULTING FROM THE DISTILLATION OF SAID STEAM-CRACKED PRODUCT INTO A THERMAL SOAKING ZONE, SUBJECTING SAID TAR BOTTOMS FRACTION TO A TEMPERATURE BETWEEN 750 AND 950*F. FOR A PERIOD OF FROM 2 TO 6 HOURS TO CONVERT SAID TAR BOTTOMS TO PITCH AND MORE VOLATILE PRODUCTS, PASSING SAID PITCH AND VOLATILE PRODUCTS TO A DISTILLATION ZONE AND THERIEN STRIPPING THE PITCH OF SUBSTANTIALLY ALL THE VIOLATE PRODUCTS BOILING BELOW ABOUTG 750*F.

References Cited (Backward Citations)

US2559285A Cited
US2764527A Cited
US2906694A Cited
US3060116A Cited
US3132090A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1969-03-14 1969-09-13 1970-03-15 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1973-03-14 1973-09-13 1974-03-15 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1977-03-14 1977-09-13 1978-03-15 $7700.00 Window Closed / Lapsed

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